[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

EP0388859B1 - Verfahren für die Aufbereitung von schlammhaltigem Wasser - Google Patents

Verfahren für die Aufbereitung von schlammhaltigem Wasser Download PDF

Info

Publication number
EP0388859B1
EP0388859B1 EP90105161A EP90105161A EP0388859B1 EP 0388859 B1 EP0388859 B1 EP 0388859B1 EP 90105161 A EP90105161 A EP 90105161A EP 90105161 A EP90105161 A EP 90105161A EP 0388859 B1 EP0388859 B1 EP 0388859B1
Authority
EP
European Patent Office
Prior art keywords
muddy water
chemical
flocs
treating
water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
EP90105161A
Other languages
English (en)
French (fr)
Other versions
EP0388859A1 (de
Inventor
Sohei Okamoto
Jiro Hirano
Takusaburo Ohnishi
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Iseki Kaihatsu Koki KK
Original Assignee
Iseki Kaihatsu Koki KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Iseki Kaihatsu Koki KK filed Critical Iseki Kaihatsu Koki KK
Priority to AT90105161T priority Critical patent/ATE80366T1/de
Publication of EP0388859A1 publication Critical patent/EP0388859A1/de
Application granted granted Critical
Publication of EP0388859B1 publication Critical patent/EP0388859B1/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material

Definitions

  • This invention relates to a muddy water treating method wherein coagulating agents are added to muddy water to be treated to coagulate fine particles in muddy water into large-sized solid flocs and more particularly, to a treating method suitably used for the process of muddy water produced by the execution of a tunnelling operation, a boring operation, a pile driving operation, an operation of removing sedimentary earth in a storage lake and sewage treatment or the like.
  • a known method of removing fine particles from muddy water comprises adding one or more coagulating agents in muddy water in a treating vessel to combine fine particles in the muddy water into flocs and sedimentating tire flocs by gravity.
  • muddy water is separated into a floc phase and an aqueous phase since the flocs are settled.
  • the thus separated flocs are removed from the treating vessel and dewatered, i.e., dehydrated, and then wasted in position. In contrast, the separated water is finally returned to rivers.
  • the coagulating agents are merely added, so that large-sized or hard flocs cannot be produced. In most case, fine particles are partially left in the liquid with the great possibility that the separated water is not transparent.
  • the formed flocs are small in size, they are liable to run away along with the liquid at the time of dewatering or transport of the flocs, thus leading to a troublesome after-treatment of the flocs.
  • the flocs are soft with their mechanical strength being small, the flocs are apt to break.
  • the flocs will be broken into fine particles, so that the broken flocs are run away along with water.
  • the opaqueness of the separated liquid means that fine particles are left in the liquid with incomplete removal of the fine particles.
  • the coagulating agents have been conventionally added in large amounts, but the use of the large amounts of expensive chemicals will require much treating costs. Even if coagulating agents are used in large amounts under conditions where the concentration of fine particles in muddy water is high, either large-sized or hard flocs are not produced or the resultant water becomes opaque.
  • GB-A 2 148 938 discloses a method for clarifying coal liquors or slurries by employing watersoluble polymers.
  • the flocculant treating agents comprise a low molecular weight polymer having a substantially high anionic character, an inorganic coflocculant and a high molecular weight polymer having a nonionic or weakly anionic character.
  • a method for treating muddy water which comprises adding a first chemical selected from the group consisting of alkali metal oxides, alkaline earth metal oxides, alkali metal hydroxides and alkaline earth hydroxides to a muddy water to be treated so as to render the pH of said muddy water to an alkaline value to deflocculate the mutually combined solids which are combined bodies of said fine particles in the muddy water; adding a second chemical containing an anionic polymer coagulant to said muddy water so as to coagulate at least a part of the deflocculated fine particles; further adding a third chemical containing a sulfate selected from a group consisting of aluminium sulfate, ferric sulfate and mixtures thereof to said muddy water to render said muddy water weakly alkaline in the pH range from about 7,0 to 7,3 and then adding a fourth chemical containing an anionic polymer coagulant to said muddy water to form a flock
  • flocs In general, fine particles in the muddy water to be treated are combined together and grow into flocs having a fair size.
  • the flocs are potentially stable, under which it is understood that when coagulants are added to the muddy water, the flocs are combined into only slightly larger-size flocs.
  • the pH of the muddy water is adjusted to an alkaline level in the pH by addition of an alkali metal oxide, alkaline earth metal oxide, alkali metal hydroxide or alkaline earth metal hydroxide, solid matters combined in the muddy water are deflocculated.
  • the muddy water is converted into a state where flocculation with polymer coagulant is effectively carried out.
  • the addition of an anionic polymer coagulant at the same time or after the conversion contributes to coagulation of part of the deflocculated fine particles and fulvic acid in the muddy water.
  • the sulfate useful in the above step includes, for example, aluminium sulfate, ferric sulfate and mixtures thereof.
  • the anionic polymer coagulants include, for example, sodium alginate, sodium polyacrylate, maleate copolymers, partial hydrolyzates of polyacrylamide and the like.
  • the anionic polymer coagulants may be used singly or in combination.
  • the pH adjusted by addition of the alkaline chemical is generally a value greater than the pH value of the muddy water by 0.5 and the pH adjusted by addition of a sulfate should,be weakly alkaline and is in the range of from 7.0 to 7.3.
  • the present invention is described by way of application examples wherein the amounts of the respective chemicals were minimized but optimum amounts which were determined according to a preliminary test from which flocs and separated water were optimumly obtained. Comparative Examples are also described.
  • a partial hydrolyzate of polyacrylamide (anionic polymer coagulant, commerical name of DK Floc DK-10 available from Kurita Kogyo Kabushiki Kaisha) having a molecular weight of about 107 was added to the muddy water as chemical 2, followed by further addition of aluminium sulfate as chemical 3 to the muddy water to adjust the pH to 7.1 to 7.3 and also of an anionic polymer coagulant used as chemical 1 to the muddy water as chemical 4.
  • the chemicals 1, 2, 3 and 4 were added as aqueous solutions with concentrations of 1.0%, 0.2%, 20% and 0.2%, respectively. During the addition of all the chemicals, the muddy water was agitated.
  • Comparative Example 1c the anionic polymer coagulant had to be added in an amount larger than in Examples 1A to 1L and Comparative Examples 1a and 1b.
  • the chemicals 1, 2 and 3 were, respectively, used as aqueous solutions having concentrations of 20%, 0.2% and 0.25%. During the addition of the respective chemicals, the muddy water were agitated.
  • Comparative Examples 2a to 2l requires larger amounts of the anionic polymer coagulant or nonionic polymer coagulant (chemical 2 or 3) than Examples 1A to 1L and Comparative Examples 1a to 1c.
  • the chemicals 1 and 2 were, respectively, added as aqueous solutions having concentrations of 20% and 0.25%. During the addition of the respective chemicals, the muddy water were agitated.
  • Comparative Examples 4a to 4l the nonionic polymer coagulant (chemical 2) had to be added in amounts larger than in Examples 1A to 1L and Comparative Examples 1a to 1c.
  • the separate waters were turbid except for Comparative Examples 4j, 4m and 4n.
  • the separated waters in Comparative Examples 4a and 4k were considerable in turbidity.
  • Comparative Examples 5a to 5o the muddy water as used in Comparative Examples 4a to 4o was treated-in the same manner as in Comparative Examples 4a to 4o except that there were used caustic soda as chemical 1 instead of aluminum sulfate and a partial hydrolyzate of polyacrylamide having a molecular weight of about 107 (anionic polymer coagulant, commercial name of DK Floc DK101 available from Kurita Kogyo Kabushiki Kaisha) as chemical 2 instead of the nonionic polymer coagulant.
  • anionic polymer coagulant commercial name of DK Floc DK101 available from Kurita Kogyo Kabushiki Kaisha
  • the chemicals 1 and 2 were added as aqueous solutions having concentrations of 1.0% and 0.2%, respectively.
  • Comparative Examples 5a, 5b, 5f to 5j and 5m to 5o the separated waters were all turbid with soft cakes.
  • Comparative Examples 5c to 5e only small-sized flocs were formed with bad solid-liquid separability.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Excavating Of Shafts Or Tunnels (AREA)
  • Physical Water Treatments (AREA)
  • Treatment Of Sludge (AREA)

Claims (5)

  1. Verfahren für die Aufbereitung von schlammhaltigem Wasser, das feine Partikel enthält, umfassend die Schritte:
    - des Zusatzes einer ersten Chemikalie, ausgewählt aus der Gruppe von Alkalimetalloxiden, Erdalkalimetalloxiden, Alkalimetallhydroxiden und Erdalkalihydroxiden zu schlammhaltigem Wasser, das so aufbereitet werden soll, daß der pH-Wert des schlammhaltigen Wassers auf einen alkalischen Wert gebracht wird, um die miteinander verbundenen Feststoffe zu entflocken, welche kombinierte Gebilde der feinen Partikel in dem schlammhaltigen Wasser sind;
    - des Zusatzes einer zweiten Chemikalie, die eine anionische, polymere, flockenbildende Substanz enthält, zu dem schlammhaltigen Wasser, um zumindest einen Teil der entflockten, feinen Partikel auszuflocken;
    - des Zusatzes einer dritten Chemikalie, die ein Sulfat enthält, ausgewählt aus einer Gruppe, bestehend aus Aluminiumsulfat, Eisensulfat und Mischungen daraus, zu dem schlammhaltigen Wasser, um das schlammhaltige Wasser schwach alkalisch zu machen mit einem pH-Wert zwischen ungefähr 7,0 und 7,3; und
    - des Zusatzes einer vierten Chemikalie, die eine anionische, polymere, flockenbildende Substanz enthält, zu dem schlammhaltigen Wasser, um eine Flocke zu bilden.
  2. Verfahren für Aufbereitung von schlammhaltigem Wasser nach Anspruch 1, wobei die anionischen, polymeren, flockenbildenden Substanzen in den zweiten und vierten Chemikalien aus der aus Natronalginat, Natronpolyacrylat, Maleatkopolymeren, Partialhydrolysaten von Polyacrylamid und Mischungen daraus bestehenden Gruppe ausgewählt werden.
  3. Verfahren für die Aufbereitung von schlammhaltigem Wasser nach Anspruch 1, wobei die ersten und zweiten Chemikalien gleichzeitig dem schlammhaltigen Wasser beigegeben werden.
  4. Verfahren für die Aufbereitung von schlammhaltigem Wasser nach Anspruch 1, wobei nach der Beigabe der ersten Chemikalie zum schlammhaltigen Wasser die zweite Chemikalie dem schlammhaltigen Wasser zugesetzt wird.
  5. Verfahren für die Aufbereitung von schlammhaltigem Wasser nach Anspruch 1, wobei die erste Chemikalie Ätznatron ist.
EP90105161A 1989-03-23 1990-03-19 Verfahren für die Aufbereitung von schlammhaltigem Wasser Expired - Lifetime EP0388859B1 (de)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT90105161T ATE80366T1 (de) 1989-03-23 1990-03-19 Verfahren fuer die aufbereitung von schlammhaltigem wasser.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP69180/89 1989-03-23
JP1069180A JPH02251294A (ja) 1989-03-23 1989-03-23 泥水の処理方法

Publications (2)

Publication Number Publication Date
EP0388859A1 EP0388859A1 (de) 1990-09-26
EP0388859B1 true EP0388859B1 (de) 1992-09-09

Family

ID=13395266

Family Applications (1)

Application Number Title Priority Date Filing Date
EP90105161A Expired - Lifetime EP0388859B1 (de) 1989-03-23 1990-03-19 Verfahren für die Aufbereitung von schlammhaltigem Wasser

Country Status (9)

Country Link
US (1) US5034137A (de)
EP (1) EP0388859B1 (de)
JP (1) JPH02251294A (de)
KR (1) KR940000557B1 (de)
CN (1) CN1045757A (de)
AT (1) ATE80366T1 (de)
AU (1) AU618456B2 (de)
CA (1) CA2012201A1 (de)
DE (1) DE69000294T2 (de)

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3829089A1 (de) * 1988-08-27 1990-03-01 Innoterv Ipari Foevallalkozo Verfahren zur abscheidung der festen phase aus fluessigen stoffen
US5614102A (en) * 1990-01-29 1997-03-25 Sakurada; Yasuyuki Method for purifying sewage
US5411149A (en) * 1992-08-11 1995-05-02 Arch Development Corporation Aqueous biphasic extraction process with pH and particle control
US5462672A (en) * 1992-08-13 1995-10-31 Chemical Grouting Co., Ltd. Process for treating sludge and system for the same
US5510037A (en) * 1993-02-12 1996-04-23 Tastayre; Gilles Regeneration of used cleaning solution
WO1994027916A1 (en) * 1993-06-01 1994-12-08 B.G. Roberts Chemicals Inc. Method of removing toxic resin acids and fatty acids from pulp and paper effluent and other streams
ES2124661B1 (es) * 1996-06-21 1999-07-01 Acideka S A Procedimiento de fabricacion de coagulantes mixtos para clarificar ag ua, coagulantes mixtos obtenidos con este procedimiento y metodo de clarificar agua con dichos coagulantes mixtos.
AU2002365283A1 (en) * 2001-11-16 2003-06-10 Technocon Gmbh Method for biological treatment of water by adding macromolecular carbohydrates
US7695630B2 (en) * 2005-11-15 2010-04-13 De Guevara Cesar Ladron Process for conditioning an aqueous solution for efficient colloidal precipitation
US20080296232A1 (en) * 2007-05-31 2008-12-04 Paul Wegner Wastewater clarifier and process
US20100140181A1 (en) 2008-12-05 2010-06-10 Gilles Tastayre Regeneration of used cleaning solution
JP5756945B2 (ja) * 2010-09-16 2015-07-29 日本ソリッド株式会社 原水の処理方法
CN107473352A (zh) * 2017-08-30 2017-12-15 杭州萧山环境投资发展有限公司 一种泥浆水快速净化的絮凝剂及其净化方法
JP2021069993A (ja) * 2019-10-31 2021-05-06 キヤノン株式会社 ウルトラファインバブル生成装置およびその制御方法

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3418237A (en) * 1963-12-22 1968-12-24 American Cyanamid Co Settling of non-argillaceous ore pulps and mineral suspensions by use of water-soluble acrylic polymers
GB1183225A (en) * 1966-03-24 1970-03-04 Simonacco Ltd Improvements in or relating to the Treatment of Slurries
US3493499A (en) * 1968-05-16 1970-02-03 Dow Chemical Co Flocculation of saline solid suspensions
US3637491A (en) * 1969-11-03 1972-01-25 Monsanto Co Clarification of water
US4173532A (en) * 1974-03-07 1979-11-06 Entenmann's, Inc. Method for treating plant effluent
JPS5399656A (en) * 1977-02-09 1978-08-31 Agency Of Ind Science & Technol Method of purifying suspended waste water
DE2802066C2 (de) * 1978-01-18 1986-05-28 Passavant-Werke AG & Co KG, 6209 Aarbergen Verfahren zur chemisch-mechanischen Aufbereitung vonGrund-, Oberflächen- oder Abwässern
JPS5584505A (en) * 1978-09-19 1980-06-25 Nippon Cement Co Ltd Sewage solid-liquid separation
JPS5670893A (en) * 1979-11-09 1981-06-13 Norihiko Base Treatment of muddy water
US4816166A (en) * 1983-10-31 1989-03-28 The Dow Chemical Company Flocculation of coal particles and coal slimes

Also Published As

Publication number Publication date
CN1045757A (zh) 1990-10-03
DE69000294D1 (de) 1992-10-15
AU618456B2 (en) 1991-12-19
ATE80366T1 (de) 1992-09-15
KR900014256A (ko) 1990-10-23
AU5147290A (en) 1990-09-27
CA2012201A1 (en) 1990-09-23
DE69000294T2 (de) 1993-01-14
US5034137A (en) 1991-07-23
EP0388859A1 (de) 1990-09-26
KR940000557B1 (ko) 1994-01-24
JPH02251294A (ja) 1990-10-09

Similar Documents

Publication Publication Date Title
EP0388859B1 (de) Verfahren für die Aufbereitung von schlammhaltigem Wasser
CA1336020C (en) Clarification process
US6267892B1 (en) Fluoride including waste water processing device and method capable of processing fluoride including waste water to have low concentration of fluoride
US5041269A (en) Recovery of alumina trihydrate in the Bayer process
CN1137307C (zh) 处理工艺用水的方法
WO1991007354A1 (en) Water treatment method
US6676840B2 (en) Fat and protein removal from process streams
JPH07136669A (ja) 溶存重金属含有排水の処理方法
US5520819A (en) Method of removing suspensions from wastewater
US5241045A (en) Process for the precipitation of aqueous plastics dispersions containing polyvinyl alcohol
US3634230A (en) Process for removal of inorganic and organic matter from waste water systems
JP2000117265A (ja) モリブデン含有排水の処理方法
US5766485A (en) Color removal from effluent waters
JPH03137987A (ja) 排水処理法
JP3339352B2 (ja) 汚泥の処理方法
US4040955A (en) Method of treating wastewater containing emulsified oils
EP0211338A2 (de) Verfahren zur Herstellung von Aluminiumoxid
JPS62277200A (ja) 汚泥の凝集処理方法
US2264790A (en) Purifying water and sewage
JPH07136408A (ja) 排水処理方法
JP2937438B2 (ja) 汚泥水の脱水方法
JPH0557292A (ja) 重金属含有廃水の処理方法
JP7240577B2 (ja) 銅イオン及び水溶性有機物含有エッチング排水の処理方法
JP2937665B2 (ja) 汚泥の凝集方法
JPH1076275A (ja) 廃水処理剤

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT CH DE FR GB IT LI NL SE

17P Request for examination filed

Effective date: 19901113

17Q First examination report despatched

Effective date: 19910508

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT CH DE FR GB IT LI NL SE

REF Corresponds to:

Ref document number: 80366

Country of ref document: AT

Date of ref document: 19920915

Kind code of ref document: T

REF Corresponds to:

Ref document number: 69000294

Country of ref document: DE

Date of ref document: 19921015

ET Fr: translation filed
ITF It: translation for a ep patent filed
PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed
PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 19940228

Year of fee payment: 5

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 19940318

Year of fee payment: 5

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: SE

Payment date: 19940329

Year of fee payment: 5

Ref country code: AT

Payment date: 19940329

Year of fee payment: 5

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 19940331

Year of fee payment: 5

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: CH

Payment date: 19940420

Year of fee payment: 5

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 19940518

Year of fee payment: 5

EAL Se: european patent in force in sweden

Ref document number: 90105161.5

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Effective date: 19950319

Ref country code: AT

Effective date: 19950319

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Effective date: 19950320

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LI

Effective date: 19950331

Ref country code: CH

Effective date: 19950331

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Effective date: 19951001

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 19950319

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19951130

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

NLV4 Nl: lapsed or anulled due to non-payment of the annual fee

Effective date: 19951001

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Effective date: 19951201

EUG Se: european patent has lapsed

Ref document number: 90105161.5

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES;WARNING: LAPSES OF ITALIAN PATENTS WITH EFFECTIVE DATE BEFORE 2007 MAY HAVE OCCURRED AT ANY TIME BEFORE 2007. THE CORRECT EFFECTIVE DATE MAY BE DIFFERENT FROM THE ONE RECORDED.

Effective date: 20050319